US1943920A - Process for the production of - Google Patents
Process for the production of Download PDFInfo
- Publication number
- US1943920A US1943920A US1943920DA US1943920A US 1943920 A US1943920 A US 1943920A US 1943920D A US1943920D A US 1943920DA US 1943920 A US1943920 A US 1943920A
- Authority
- US
- United States
- Prior art keywords
- hydrochloric acid
- magnesium
- chlorine
- magnesium chloride
- chloride
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 18
- 238000004519 manufacturing process Methods 0.000 title description 9
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 65
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 54
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 29
- 239000011777 magnesium Substances 0.000 description 29
- 229910052749 magnesium Inorganic materials 0.000 description 29
- 229910001629 magnesium chloride Inorganic materials 0.000 description 27
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 23
- 239000000460 chlorine Substances 0.000 description 23
- 229910052801 chlorine Inorganic materials 0.000 description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 20
- XTEGARKTQYYJKE-UHFFFAOYSA-M Chlorate Chemical compound [O-]Cl(=O)=O XTEGARKTQYYJKE-UHFFFAOYSA-M 0.000 description 12
- YGYAWVDWMABLBF-UHFFFAOYSA-N Phosgene Chemical compound ClC(Cl)=O YGYAWVDWMABLBF-UHFFFAOYSA-N 0.000 description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 12
- 239000001301 oxygen Substances 0.000 description 12
- 229910052760 oxygen Inorganic materials 0.000 description 12
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 8
- 238000005868 electrolysis reaction Methods 0.000 description 8
- 125000004122 cyclic group Chemical group 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000018044 dehydration Effects 0.000 description 6
- 238000006297 dehydration reaction Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 150000002927 oxygen compounds Chemical class 0.000 description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 5
- 229910052739 hydrogen Inorganic materials 0.000 description 5
- 239000000395 magnesium oxide Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 239000003575 carbonaceous material Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 230000001131 transforming effect Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000010981 drying operation Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 229960004424 carbon dioxide Drugs 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 235000012254 magnesium hydroxide Nutrition 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
- C25C3/04—Electrolytic production, recovery or refining of metals by electrolysis of melts of magnesium
Definitions
- This invention relates to a process for the prep aration of metallic magnesium.
- the anhydrous chloride of magnesium is electrolyzed in a molten state and the chlorine coming from the electrolyzing vats is brought into contact with a milk of magnesia, so that the oxide of magnesium is decomposed and that chloride of magnesium and chlorate of magnesium are formed simultaneously.
- the chloride of magnesium is then separated from the chlorate by crystallization of the chloride, and the chloride, after dehydration, is electrolyzed in the molten state.
- Magnesium chloride has also been obtained starting with magnesia by the action of carbon tetrachloride, by liberating carbon oxychloride which likewise reacts upon the magnesia.
- the chloride of magnesium obtained in any suitable manner can be dehydrated in the presence of hot nascent hydrochloric acid, for example by burning chlorine .and hydrogen at their meeting point in the vessel containing the magnesium chloride to be dehydrated.
- the object of the present invention is a new process for the preparation of metallic magnesium which permits all formation of the chlorate to be avoided. 4
- This fundamental cycle may be completed by the addition of complementary operations.
- all or a part of the hydrochloric acid formed may be employed for the preliminary dehydration of the chloride of magnesium treated, the hydrochloric acid recovered at the end of the drying operations being subsequently reintroduced into the cycle.
- hydrochloric acid will be produced by one of the following methods.
- the chlorine accompanied by a suitable amount of oxygen, will be transformed, by contact with a suitable fuel, into phosgene, COClz.
- phosgene Upon treatment with water, the phosgene will produce hydrochloric acid and carbonic anhydride, giving the well known reactions.
- the hydrochloric acid may be produced by direct synthesis, by the various known methods, electrlc or catalytic.
- the chlorine produced by electrolysis, (which is always mixed with more or less air or oxygen, on account of the well known fact that it is very difficult in practice to construct vats which are air tight), is passed over coal or coke brought to a red heat in a suitable container.
- the mixture of air. and chlorine must contain at least one volume of oxygen for two of chlorine and if required a further quantity of fresh air is added to the chlorine from the cells, to give at least this ratio.
- the phosgene is then brought into contact with water, either in the liquid state, previously heated, or in the state of steam, which water is either pure or mixed with othersubstances, such for example as hydrochloric acid.
- water is either pure or mixed with othersubstances, such for example as hydrochloric acid.
- the hydrochloric'acid thus'formed is brought into contactwith magnesia or'with magnesium carbonate to form the magnesium chloride, and
- cycle forming the subject of the present invention may be combined to a certain extent with the various cycles employed up to the present, by allowing a certain amount of chlorate, for example, to form and partially by employing the chlorine for transforming it into hydrochloric acid as described above.
- hydrochloric acid may be em ployed simultaneously in the desired proportions, In this case a part of the chlorine is passed over the red hot coal while the other passes directly into electric or catalytic apparatus in which it has to combine with the hydrogen.
- the cyclic process for the manufacture of magnesium by the electrolysis of fused magnesium chloride which comprises the steps of bringing the chlorine which is liberated at the anode of the electrolytic vessel with oxygen, into contact with a material containing carbon at a temperature sufficiently elevated to form phosgene, adding water to the phosgene thus obtained to produce hydrochloric acid gas, reacting with the hydrochloric acid gas thus obtained upon an oxygen compound of magnesium to transform it into magnesium chloride.
- the cyclic process for the manufacture of magnesium which comprises the sequence of steps, viz:the electrolysis of fused magnesium chloride, then reacting with the chlorine which liberated at the anode of the electrolysis of the magnesium chloride and with oxygen upon a material containing carbon at a temperature adapted to form phosgene, adding water to the phosgene thus obtained in such proportions as to form hydrochloric acid gas, dehydrating magnesium chloride by the hydrochloric acid gas thus obtained, and acting with the hydrochloric acid gas thus charged with water upon an oxygen compound of magnesium to transform it into magnesium chloride, which is afterwards dehydrated as explained above by the hydrochloric acid gas, and is thereafter used in the electrolytic step first mentioned.
- a process of producing magnesium by a process which includes a double counter progression of materials as follows: (a1) introducing magnesia into contact with hydrochloric acid and Water to form magnesium chloride in a wet condition, (a2) drying the magnesium chloride by heat in contact with a current of hot, substantially dry hydrochloric acid gas, then (a3) subjecting the dried magnesium chloride to electrolysis to produce magnesium and chlorine, (b1) converting the chlorine from step (a3) into hydrochloric acid gas, (b2) passing such hydrochloric acid gas into the step (a2) to dry the magnesium chloride and to moisten the hydrochloric acid gas, (b3) passing such moistened hydrochloric acid into step ((11) to produce wet magnesium chloride, said step of converting the chlorine into hydrochloric acid being performed by passing the chlorine, together with oxygen in amount equal to at least one-half the absolute volume of chlorine, through a heated space in contact with hot carbonaceous fuel, to form phosgene, and treating the phosgene with water not
- the cyclic process for the manufacture of magnesium by the electrolysis of fused magnesium chloride which comprises the steps of bringing the chlorine which is liberated at the anode of the electrolytic vessel, with oxygen into contact with a material containing carbon at an elevated temperature, adding water only in such an amount to obtain hydrochloric acid gas in a substantially dry state, heating wet magnesium chloride in such substantially dry hydrochloric acid gas, and reacting with the hydrochloric acid upon an oxygen compound of magnesium to transform it into magnesium chloride.
- the cyclic process for the manufacture of magnesium which comprises electrolysis of fused magnesium chloride, bringing the chlorine which is liberated at the anode of the electrolytic vessel, with oxygen, into contact with a material containing carbon at an elevated temperature, adding a mixture of liquid water and steam to obtain hydrochloric acid gas while controlling the proportions of water and steam so as to maintain the temperature of reaction below that at which the slag from the carbonaceous material would fuse, and controlling the total amount of water and steam to such proportions as will give substantially dry HCl gas, heating magnesium chloride containing water, in an atmosphere of said substantially dry HCl gas, sufficiently to dehydrate the MgClz, whereby wet hydrochloric acid is produced, and reacting with the wet hydrochloric acid thus obtained upon an oxygen compound of magnesium to transform it into magnesium chloride.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
Patented Jan. 16, 1934 PROCESS FOR THE PRODUCTION OF METALLIC MAGNESIUM Maurice Noel Lacell, Finchley, London, England No Drawing. Application March 21, 1927, Serial No. 177,225, and in France March 26, 1926.
Renewed May 29, 1933 '1 Claims.
This invention relates to a process for the prep aration of metallic magnesium.
The known cyclic processes for the preparation of metallic magnesium usually employ the following sequence of operations:
The anhydrous chloride of magnesium is electrolyzed in a molten state and the chlorine coming from the electrolyzing vats is brought into contact with a milk of magnesia, so that the oxide of magnesium is decomposed and that chloride of magnesium and chlorate of magnesium are formed simultaneously.
The chloride of magnesium is then separated from the chlorate by crystallization of the chloride, and the chloride, after dehydration, is electrolyzed in the molten state.
In practice, when it is desired to work with large quantities, the chlorate of magnesium produced represents a great loss of chlorine and magnesia.
Magnesium chloride has also been obtained starting with magnesia by the action of carbon tetrachloride, by liberating carbon oxychloride which likewise reacts upon the magnesia.
The chloride of magnesium obtained in any suitable manner can be dehydrated in the presence of hot nascent hydrochloric acid, for example by burning chlorine .and hydrogen at their meeting point in the vessel containing the magnesium chloride to be dehydrated.
The object of the present invention is a new process for the preparation of metallic magnesium which permits all formation of the chlorate to be avoided. 4
It consists essentially in transforming the chlorine into hydrochloric acid by any suitable method, in then causing the hydrochloric acid formed, to act upon the oxide of magnesium or the carbonate of magnesium so that only the chloride of magnesium is formed to the exclusion of the chlorate.
This fundamental cycle may be completed by the addition of complementary operations. For instance, all or a part of the hydrochloric acid formed may be employed for the preliminary dehydration of the chloride of magnesium treated, the hydrochloric acid recovered at the end of the drying operations being subsequently reintroduced into the cycle.
Preferably the hydrochloric acid will be produced by one of the following methods.
The chlorine, accompanied by a suitable amount of oxygen, will be transformed, by contact with a suitable fuel, into phosgene, COClz. Upon treatment with water, the phosgene will produce hydrochloric acid and carbonic anhydride, giving the well known reactions.
In the case when free hydrogen is available, the hydrochloric acid may be produced by direct synthesis, by the various known methods, electrlc or catalytic.
By way of example and in order to make the description more clear, certain special modes of carrying the invention into effect are described hereinafter.
The chlorine, produced by electrolysis, (which is always mixed with more or less air or oxygen, on account of the well known fact that it is very difficult in practice to construct vats which are air tight), is passed over coal or coke brought to a red heat in a suitable container. The mixture of air. and chlorine must contain at least one volume of oxygen for two of chlorine and if required a further quantity of fresh air is added to the chlorine from the cells, to give at least this ratio.
Upon contact with the red hot coal phosgene is formed according to the equation:
The phosgene is then brought into contact with water, either in the liquid state, previously heated, or in the state of steam, which water is either pure or mixed with othersubstances, such for example as hydrochloric acid. The following well known reaction takes place. The term water as used in the appended claims is intended to include both water in the liquid state as well as water in the form of steam.
ing from these various reactions, some 'undecom-' posed carbon ,monoxide;.; It has no effect. upon 7 the subsequent reactionsofthe'cycle.
The hydrochloric'acid thus'formed is brought into contactwith magnesia or'with magnesium carbonate to form the magnesium chloride, and
the cycle continues.
Instead of proceeding by way of phosgene, it is possible, when pure hydrogen is available, to produce the necessary hydrochloric acid by direct combination, by means of any known process, electric or catalytic, for example. Either the quantity of hydrogen strictly necessary for transforming the chlorine into hydrochloric acid may be used, or the excess amount which is sunicient in order to burn out the oxygen and form water. It is advantageous to burn out the oxygen when it is intended to employ the hydrochloric acid for effecting a preliminary drying of the magnesium chloride for there is a danger of the residual oxy'- genreacting upon the hydrochloric acid during this drying operation according to the reaction:
It is to be noted that the cycle forming the subject of the present invention may be combined to a certain extent with the various cycles employed up to the present, by allowing a certain amount of chlorate, for example, to form and partially by employing the chlorine for transforming it into hydrochloric acid as described above.
Further, the two methods for the production of hydrochloric acid described above may be em ployed simultaneously in the desired proportions, In this case a part of the chlorine is passed over the red hot coal while the other passes directly into electric or catalytic apparatus in which it has to combine with the hydrogen.
I claim:
1. The cyclic process for the manufacture of magnesium by the electrolysis of fused magnesium chloride, which comprises the steps of bringing the chlorine which is liberated at the anode of the electrolytic vessel with oxygen, into contact with a material containing carbon at a temperature sufficiently elevated to form phosgene, adding water to the phosgene thus obtained to produce hydrochloric acid gas, reacting with the hydrochloric acid gas thus obtained upon an oxygen compound of magnesium to transform it into magnesium chloride.
2. The cyclic process for the manufacture of magnesium which comprises the sequence of steps, viz:the electrolysis of fused magnesium chloride, then reacting with the chlorine which liberated at the anode of the electrolysis of the magnesium chloride and with oxygen upon a material containing carbon at a temperature adapted to form phosgene, adding water to the phosgene thus obtained in such proportions as to form hydrochloric acid gas, dehydrating magnesium chloride by the hydrochloric acid gas thus obtained, and acting with the hydrochloric acid gas thus charged with water upon an oxygen compound of magnesium to transform it into magnesium chloride, which is afterwards dehydrated as explained above by the hydrochloric acid gas, and is thereafter used in the electrolytic step first mentioned.
3. A process of producing magnesium by a process which includes a double counter progression of materials, as follows: (a1) introducing magnesia into contact with hydrochloric acid and Water to form magnesium chloride in a wet condition, (a2) drying the magnesium chloride by heat in contact with a current of hot, substantially dry hydrochloric acid gas, then (a3) subjecting the dried magnesium chloride to electrolysis to produce magnesium and chlorine, (b1) converting the chlorine from step (a3) into hydrochloric acid gas, (b2) passing such hydrochloric acid gas into the step (a2) to dry the magnesium chloride and to moisten the hydrochloric acid gas, (b3) passing such moistened hydrochloric acid into step ((11) to produce wet magnesium chloride, said step of converting the chlorine into hydrochloric acid being performed by passing the chlorine, together with oxygen in amount equal to at least one-half the absolute volume of chlorine, through a heated space in contact with hot carbonaceous fuel, to form phosgene, and treating the phosgene with water not in substantial excess.v
4. The cyclic process for the manufacture of magnesium by the electrolysis of fused magnesium chloride, which comprises the steps of bringing the chlorine which is liberated at the anode of the electrolytic vessel, with oxygen into contact with a material containing carbon at an elevated temperature, adding water only in such an amount to obtain hydrochloric acid gas in a substantially dry state, heating wet magnesium chloride in such substantially dry hydrochloric acid gas, and reacting with the hydrochloric acid upon an oxygen compound of magnesium to transform it into magnesium chloride.
5. The cyclic process for the manufacture of magnesium, which comprises electrolysis of fused magnesium chloride, bringing the chlorine which is liberated at the anode of the electrolytic vessel, with oxygen, into contact with a material containing carbon at an elevated temperature, adding a mixture of liquid water and steam to obtain hydrochloric acid gas while controlling the proportions of water and steam so as to maintain the temperature of reaction below that at which the slag from the carbonaceous material would fuse, and controlling the total amount of water and steam to such proportions as will give substantially dry HCl gas, heating magnesium chloride containing water, in an atmosphere of said substantially dry HCl gas, sufficiently to dehydrate the MgClz, whereby wet hydrochloric acid is produced, and reacting with the wet hydrochloric acid thus obtained upon an oxygen compound of magnesium to transform it into magnesium chloride.
6. The cyclic process for the manufacture of magnesium by the following stepszelectrolysis of fused magnesium chloride, sending the chlorine which is liberated at the anode of the electrolytic vessel with oxygen into contact with a material containing carbon at an elevated temperature, adding water to obtain hydrochloric acid gas, utilizing the hydrochloric acid gas so formed for the dehydration of partially hydrated magnesium chloride and reacting with the hydrochloric acid remaining after said dehydration step upon an oxygen compound of magnesium to transform it into magnesium chloride.
7. The cyclic process for the manufacture of magnesium by the following steps:electrolysis of fused magnesium chloride, sending the chlorine which is liberated at the anode of the electrolytic vessel with oxygen into contact with a hot carbonaceous material, adding a mixture of liquid water and steam to obtain hydrochloric acid gas, controlling the proportions of water and steam so as to maintain the temperature of reaction below that at which the slag from the carbonaceous material would fuse, utilizing the hydrochloric acid gas so formed for the dehydration of partially hydrated magnesium chloride and reacting with the hydrochloric acid after the said dehydration step upon an oxygen compound of magnesium to transform it into magnesium chloride. MAURICE NOEL LACELL.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1943920A true US1943920A (en) | 1934-01-16 |
Family
ID=3426075
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US1943920D Expired - Lifetime US1943920A (en) | Process for the production of |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1943920A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2832670A (en) * | 1954-01-13 | 1958-04-29 | Bayer Ag | Process for the decomposition of phosgene |
| US4943426A (en) * | 1988-06-20 | 1990-07-24 | Aluminum Company Of America | Method for regulating reaction temperature |
-
0
- US US1943920D patent/US1943920A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2832670A (en) * | 1954-01-13 | 1958-04-29 | Bayer Ag | Process for the decomposition of phosgene |
| US4943426A (en) * | 1988-06-20 | 1990-07-24 | Aluminum Company Of America | Method for regulating reaction temperature |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US1743080A (en) | Manufacture of pulp and treatment of residual liquors, etc. | |
| US1943920A (en) | Process for the production of | |
| US1147832A (en) | Production of aluminum chlorid. | |
| US1979151A (en) | Manufacture of alkali carbonate or alkali hydroxide | |
| US956120A (en) | Process of producing manganates, permanganates, halogens, and hydroxids. | |
| US1528319A (en) | Process for the preparation of oxygenated compounds of titanium and pigments containing said compounds | |
| US2216402A (en) | Method of producing pure magnesium compounds | |
| US2974093A (en) | Process for the manufacture of salt mixtures for the electrolytic production of magnesium | |
| US1115776A (en) | Producing hydrogen. | |
| US1489525A (en) | Manufacture of magnesium chloride | |
| US474539A (en) | Walter walker | |
| USRE15314E (en) | Island | |
| US1458651A (en) | Process for the production of calcium chloride | |
| US2201206A (en) | Production of anhydrous magnesium chloride | |
| US724251A (en) | Process of producing sulfuric acid and metallic oxids. | |
| US1923594A (en) | Process for producing anhydrous nonvolatile metal chlorides | |
| US1498833A (en) | Process for the production of magnesium chloride | |
| US376409A (en) | Adolf kaysee | |
| US1584597A (en) | Process of making sodium sulphide | |
| US2221356A (en) | Manufacture of alkall phosphates | |
| US1661894A (en) | Manufacture of anhydrous magnesium chloride | |
| GB268316A (en) | A process for the production of metallic magnesium | |
| US1166524A (en) | Process of purifying electrolytic chlorin. | |
| US1040977A (en) | Process for producing hydrochloric acid and alkali-silico-aluminates. | |
| US1331688A (en) | Production and utilization of magnesium chlorid |